US5122545A - Production method of prefoamed synthetic resin particles - Google Patents
Production method of prefoamed synthetic resin particles Download PDFInfo
- Publication number
- US5122545A US5122545A US07/617,578 US61757890A US5122545A US 5122545 A US5122545 A US 5122545A US 61757890 A US61757890 A US 61757890A US 5122545 A US5122545 A US 5122545A
- Authority
- US
- United States
- Prior art keywords
- resin particles
- blowing agent
- temperature
- vessel
- inorganic gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/22—After-treatment of expandable particles; Forming foamed products
- C08J9/228—Forming foamed products
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
Definitions
- the present invention relates to a production method of prefoamed synthetic resin particles.
- a process has conventionally been known, in which resin particles with a volatile blowing agent contained therein is dispersed in a dispersing medium such as water within a closed vessel, the resulting dispersion is heated to a temperature at least equal to the softening temperature of the resin particles with the internal pressure of the vessel being held at least equal to the vapor pressure of the blowing agent, thereby impregnating the resin particles with the blowing agent, and the vessel is opened at one end thereof to release the thus-impregnated resin particles and the dispersing medium into an atmosphere having a pressure lower than that inside the vessel, whereby the resin particles are allowed to undergo foaming.
- a dispersing medium such as water within a closed vessel
- Exemplary volatile blowing agents useful in the practice of the above process primarily include hydrocarbons such as propane, butane and pentane; and halogenated hydrocarbons such as trichlorofluoromethane and dichloro-difluoromethane.
- hydrocarbons such as propane, butane and pentane
- halogenated hydrocarbons such as trichlorofluoromethane and dichloro-difluoromethane.
- many of compounds employed as these volatile blowing agents however involve problems such as toxicity, inflammability and/or the like or the problem of ozonosphere destruction like flons or, even if rather free of serious problems from the standpoint of hazards or environmental destruction, the problem that the price is too high to permit commercial use.
- a volatile blowing agent induces swelling of resin particles, thereby restricting the appropriate foaming temperature range upon foaming. As a result, the foaming temperature gives greater influence to the expansion ratio, leading to the problem that control of the expansion ratio becomes difficult.
- blowing agent of the inorganic gas type however involves the problem that it hardly permits high-temperature foaming and hence the production of a foamed product having a high expansion ratio, because the blowing agent has poor impregnation property into resin particles and, moreover, secondary crystallization of the resin particles can be scarcely promoted.
- a blowing agent of the inorganic gas type is also accompanied by the problem that the reduction of expansion ratio becomes more conspicuous along the passage of time from the initiation of foaming, for example, an expansion ratio of about 20-30 times in the beginning of a foaming operation may decrease to an expansion ratio of about 10 times near the end of the foaming operation, resulting in substantial variations in expansion ratio.
- the present inventors have proceeded with a further extensive investigation to overcome the above problems.
- the present inventors have found a process which permits the provision of prefoamed particles of a high expansion ratio even when they are produced on an industrial scale by using a blowing agent of the inorganic gas type and which, when a conventional volatile blowing agent is used, allows to reduce the amount of the blowing agent to be employed and permits the provision of prefoamed particles of a high expansion ratio still more stably than the process disclosed in Japanese Patent Application Laid-Open No. 4738/1986, leading to the completion of the present invention.
- foamable resin particles in a dispersing medium within a closed vessel, said foamable resin particles containing a water-soluble inorganic substance and a blowing agent therein;
- the present invention has numerous advantages. Since the foamable resin particles containing the water-soluble inorganic substance and the blowing agent are caused to undergo foaming in the process of the present invention, prefoamed particles of a high expansion ratio can be obtained easily even when a blowing agent of the inorganic gas type is used.
- a volatile blowing agent is used, the process of the present invention makes it possible to reduce the amount of the volatile blowing agent to be used compared to the conventional processes which also make use of a similar volatile blowing agent and hence to permit the production of prefoamed particles of a high expansion ratio even when the volatile blowing agent is used in a small amount.
- An inorganic gas can be used as the blowing agent.
- the same inorganic gas as the blowing agent or a mixed gas of the same inorganic gas as the blowing agent and another inorganic gas may be fed into the vessel to apply a back pressure so that the foaming can be conducted while maintaining the internal pressure of the vessel at a level at least equal to the prefoaming partial pressure of the blowing agent inside the vessel.
- prefoamed particles obtained near the end of a foaming operation may differ significantly in expansion ratio from those obtained shortly after the initiation of the foaming operation immediately, thereby making it possible to produce excellent prefoamed particles throughout the foaming operation.
- the resin particles are held at their foaming temperature for a while after the same inorganic gas as the blowing agent or the mixed gas of the same inorganic gas as the blowing agent and another inorganic gas has been fed into the vessel in the above process, the prefoamed particles can be obtained with a still greater expansion ratio.
- the oxidative deterioration of the resin particles and hence the prefoamed resin particles can be minimized even when an oxygen-bearing inorganic gas is used as the inorganic gas.
- FIG. 1 is a diagram showing a DSC curve of prefoamed particles containing secondary crystals therein;
- FIG. 2 is a diagram showing a DSC curve of prefoamed particles containing no secondary crystals therein.
- Exemplary resin particles usable in the present invention include particles of polypropylene resins such as propylene homopolymer, propylene-ethylene random copolymers, propylene-ethylene block copolymers, propylene-butene random copolymers, propylene-ethylene-butene random copolymers, etc.; and particles of polyethylene resins such as high-density polyethylene, low-density polyethylene, linear low-density polyethylenes, etc. which are copolymers of ethylene with small amounts of ⁇ -olefins (carbon numbers: 4, 6, 8, etc.).
- polypropylene resins such as propylene homopolymer, propylene-ethylene random copolymers, propylene-ethylene block copolymers, propylene-butene random copolymers, propylene-ethylene-butene random copolymers, etc.
- polyethylene resins such as high-density polyethylene, low-density polyethylene, linear low-density polyethylenes,
- polypropylene resins--such as propylene-ethylene random copolymers, propylene-butene random copolymers and propylene-ethylene-butene random copolymers--and linear low-density polyethylenes are preferred. Although these resins may be crosslinked, uncrosslinked resins are particularly preferred.
- the water-soluble inorganic substance has a solubility of at least 1 g per 100 g of water of 40.C, with 5 g or higher being especially preferred.
- Illustrative of the water-soluble inorganic substance include borax, nickel sulfate, manganese sulfate, sodium chloride, magnesium chloride, calcium chloride, etc. Among these, borax is preferred. These inorganic substances can be used either singly or in combination.
- Each inorganic substance can be incorporated in resin particles by kneading it in a molten resin, extruding the resultant mass into strands, quenching the strands and then pelletizing the quenched strands.
- the inorganic substance is usually added in the form of powder, but not particular limitation is imposed on its average particle size. It is however generally preferred to use a water-soluble inorganic substance having an average particle size of 0.1-150 ⁇ m, notably 1-100 ⁇ m. It is preferable to add one or more of these water-soluble inorganic substances in a total amount such that their total content in the resin particles ranges from 0.01 wt.% to 2 wt.%, especially from 0.02 wt.% to 1 wt.%.
- the preferable average particle size of the resin particles containing such inorganic substance or substances is generally 0.3-5 mm with 0.5-3 mm being especially preferred.
- the step in which the resin particles are impregnated with the blowing agent may be either before or after the step in which the resin particles are dispersed in the dispersing medium within the closed vessel.
- the impregnation of the resin particles is however carried out in the course of the step in which the resin particles are dispersed in the dispersing medium and is heated to their foaming temperature.
- the resin particles can be impregnated with the blowing agent, after once dissolving or dispersing the blowing agent in the dispersing medium.
- the resin particles can be impregnated, for example, by charging the resin particles, the blowing agent and the dispersing medium in a closed vessel and then heating and pressurizing them under stirring.
- Blowing agents useful in the present invention include volatile blowing agents such as propane, butane, pentane, hexane, cyclobutane, cyclohexane, trichlorofluoromethane dichlorodifluoromethane monochlorodifluoromethane, 1-chloro-1,1-difluoroethane, 1,1,1,2-tetrachloroethane 1,1-dichloro-2,2,2-trifluoroethane, 1,1,1-difluoroethane and 1-chloro-1,2,2,2-tretrafluoroethane; and blowing agents of the inorganic gas type such as nitrogen, carbon dioxide, argon, air or the like. Among these, nitrogen, carbon dioxide and air are particularly preferred. When these blowing agents of the inorganic gas type are used, it is preferable to feed them to raise the internal pressure of the vessel to 20-50 kg/cm 2 ⁇ G.
- Any dispersing medium can be used to disperse the resin particles as long as it does not dissolve the resin particles.
- the dispersing medium include water, ethylene glycol, glycerin, methanol, ethanol and the like. Water is usually employed.
- a fusion-bonding preventive can be used to prevent fusion-bonding of the resin particles.
- Any fusion-bonding preventive can be used regardless of whether it is inorganic or organic, so long as it is not dissolved in a dispersing medium such as water and is not molten under heat.
- Inorganic fusion-bonding preventives are generally preferred.
- Illustrative inorganic fusion-bonding preventives include aluminum oxide, titanium oxide, aluminum hydroxide, basic magnesium carbonate, basic zinc carbonate, calcium carbonate, tricalcium phosphate, and magnesium pyrophosphate.
- fusion-bonding preventives in combination with an emulsifier.
- the emulsifier include anionic surfactants such as sodium dodecylbenzenesulfonate and sodium oleate.
- anionic surfactants such as sodium dodecylbenzenesulfonate and sodium oleate.
- the fusion-bonding preventive those having an average particle size of 0.001-100 ⁇ m, especially 0.001-30 ⁇ m are preferred.
- the fusion-bonding preventive can be added preferably in an amount of 0.01-10 parts by weight per 100 parts by weight of the resin particles.
- the emulsifier can be added generally in an amount of 0.001-5 parts by weight per 100 parts by weight of the resin particles.
- the inclusion of secondary crystals in the foamable resin particles is preferred.
- Prefoamed particles which have been obtained from foamable resin particles containing these secondary crystals have excellent moldability.
- the inclusion of secondary crystals in foamable resin particles is advantageous especially when the resin particles are made of a uncrosslinked polypropylene resin such as a propylene-ethylene random copolymer or an uncrosslinked linear low-density polyethylene resin.
- the existence of secondary crystals can be determined by whether or not a high-temperature peak on a side higher in temperature than an inherent peak attributed to endotherm upon so-called melting of the resin appears on a DSC curve obtained by differential scanning calorimetry of the resulting prefoamed particles.
- the inherent peak and high-temperature peak can each be determined by performing differential scanning calorimetry of the same sample twice.
- 1-10 mg of a sample (resin) is heated first to 220° C. at 10° C./min by a differential scanning calorimeter to obtain a first DSC curve.
- the sample is next cooled down from 220° C. to about 40° C. at a rate of 10° C./min and is again heated to 220° C. at 10° C./min, thereby obtaining a second DSC curve.
- the inherent peak and the high-temperature peak can be distinguished from each other.
- the inherent peak is an endothermic peak caused by so-called melting of the resin, it appears on both the first DSC curve and the second DSC curve.
- the highest temperature of the inherent peak may vary somewhat between the first measurement and the second measurement in some instances. The difference is however smaller than 5° C, usually not greater than 2° C.
- the high-temperature peak indicates an endothermic peak which appears on a side higher in temperature than the inherent peak on the first DSC curve. The existence of secondary crystals can be confirmed by the appearance of the high-temperature peak. When no substantial high-temperature peak appears, it is judged that no secondary crystals exist.
- the preferable temperature difference therebetween is at least 5° C. with 10° C. or greater being particularly preferred.
- FIGS. 1 and 2 show DSC curves obtained by differential scanning calorimetry of prefoamed particles.
- FIG. 1 corresponds to prefoamed particles containing secondary crystals and FIG. 2 to prefoamed particles free of secondary crystals.
- Curves 1 and 2 are DSC curves obtained by the first measurement
- Curves 1' and 2' are DSC curves obtained by the second measurement.
- a high-temperature peak A which is not seen on Curve 1' obtained by the second measurement has appeared in addition to Inherent Peak B (Inherent Peak B' only appears on Curve 1' obtained by the second measurement).
- prefoamed particles containing secondary crystals as shown by Curve 1 can be produced, for example, by a process as will be described next.
- a uncrosslinked polypropylene resin such prefoamed particles can be obtained generally by holding resin particles at a temperature at least equal to (their melting point minus 20° C.) or so but lower than their melting completion temperature for a sufficient time, usually for 5-90 minutes, preferably for 15-60 minutes in a pressure vessel without raising the temperature of the resin particles to their melting completion temperature or higher.
- resin particles In the case of an uncrosslinked linear low-density polyethylene on the other hand, it is usually necessary to hold resin particles at a temperature at least equal to (their melting point minus 15° C.) or so but lower than their melting completion temperature for a sufficient time, generally for 5-90 minutes, preferably for 5-30 minutes in a pressure vessel without raising the temperature of the resin particles to their melting completion temperature or higher.
- the resin particles used in the above heating step may be foamable resin particles in which a blowing agent has already been incorporated, resin particles may be impregnated with the blowing agent concurrently with their heating in the heating step.
- prefoamed particles having good moldability can still be obtained even when the foaming temperature upon releasing the thus-heated foamable resin particles into an atmosphere having a pressure lower than that inside the vessel to allow them to undergo foaming (i.e., the temperature at the time of releasing) is equal to or higher than their melting completion temperature, so long as the foaming temperature is a temperature not higher than the high-temperature peak described above.
- the holding temperature in each sub-step is controlled higher than that in the preceding sub-step It is desirable to set the holding temperature of the last sub-step equal to the foaming temperature.
- the foaming temperature at which the foamable resin particles and the dispersing medium are released into an atmosphere having a pressure lower than that inside the vessel to allow the foamable resin particles to undergo foaming is a least equal to the softening temperature
- a temperature around the melting point is however particularly preferred.
- the preferred foaming temperature range varies depending on the kind of the resin.
- a temperature range at least equal to (the melting point minus 5.C.) but not higher than (the melting point plus 15° C.) especially a temperature range at least equal to (the melting point minus 3° C.) but not higher than (the melting point plus 10° C.) is preferred.
- a temperature range at least equal to (the melting point minus 10° C.) but not higher than (the melting point plus 5° C.) is preferred.
- the heating rate upon heating the resin particles to their foaming temperature is preferably 114 10° C./min, with 2-5° C./min being especially preferred.
- the pressure of the atmosphere may be any pressure lower than that inside the vessel but is the atmospheric pressure in general.
- foamable resin particles Under a pressure that prevents their foaming inside the vessel, generally at an elevated pressure of 5 kg/cm 2 ⁇ G or higher.
- foamable resin particles In some conventional processes in which foamable resin particles are released into an atmosphere having a pressure lower than that inside the vessel to allow them to undergo foaming, it is attempted to stabilize the expansion ratio by holding foamable resin particles at foaming temperature for a while and then releasing them from the vessel by applying a back pressure with nitrogen gas while maintaining the internal pressure of the vessel at a level equal to or higher than the vapor pressure of an associated blowing agent.
- blowing agent of the inorganic gas type typically carbon dioxide is used and foamable resin particles are released for their foaming into an atmosphere having a pressure lower than that inside the vessel while applying a back pressure with nitrogen gas alone as in the conventional foaming processes, the expansion ratio of the resulting prefoamed particles decreases considerably as time goes on from the initiation of the release.
- Use of a blowing agent of the inorganic gas type as a blowing agent therefore requires to conduct the foaming while applying a back pressure with the same inorganic gas as the inorganic gas employed as a blowing agent or with a mixed gas of the same inorganic gas and another inorganic gas.
- the blowing agent is a mixed gas such as air
- the same inorganic gas as the blowing agent said same inorganic gas being employed to apply the back pressure
- the blowing agent is air by way of example, it is possible to use air, nitrogen, an air/nitrogen mixed gas or the like as the same inorganic gas as the blowing agent.
- carbon dioxide is employed as a blowing agent, it is preferable to use nitrogen, air, argon or the like as another inorganic gas different from the inorganic gas employed as the blowing agent.
- the mixing ratio of the same inorganic gas as the blowing agent to another inorganic gas may preferably range from 3:7 to 9.5:0.5 by weight.
- This mixed gas is supplied such that the internal pressure of the vessel is maintained at a level at least equal to the prefoaming partial pressure of the blowing agent of the inorganic gas type inside the vessel throughout the step in which the resin particles are released. If the internal pressure of the vessel during the foaming is lower than the partial pressure of the blowing agent of the inorganic gas type inside the vessel before the foaming, the expansion ratio of the resulting prefoamed particles gradually becomes smaller although this decrease of the expansion ratio varies depending on the level of the internal pressure of the vessel during the foaming.
- the preferred pressure range of a mixed gas to be fed to apply a back pressure is 10-50 kg/cm 2 ⁇ G when its mixing ratio falls within the range specified above.
- a blowing agent of the inorganic gas type it is preferable to perform foaming by impregnating resin particles with the blowing agent within a vessel, feeding the same inorganic gas as the blowing agent or a mixed gas of the same inorganic gas and another inorganic gas different from the blowing agent, said former same inorganic gas or said another inorganic gas having a pressure at least equal to the partial pressure of the blowing agent in the vessel, into the vessel and once holding the thus-impregnated resin particles at their foaming temperature, and then releasing the resulting resin particles from the vessel while applying a back pressure as described above.
- the another inorganic gas as employed here is similar to the another inorganic gas employed in the above-described mixed gas and is different from the inorganic gas employed as the blowing agent.
- the blowing agent is carbon dioxide
- the term "another inorganic gas" means an inorganic gas other than carbon dioxide. In this process, it is desirable to feed the same inorganic gas as the blowing agent or the mixed gas of the same inorganic gas as the blowing agent and another inorganic gas immediately after raising the internal temperature of the vessel to the foaming temperature.
- the most desirable embodiment of this process comprises applying a predetermined back pressure immediately after the internal temperature of the vessel has been raised to the foaming temperature, maintaining resin particles for a while under the same conditions to promote further impregnation of the resin particles with the same inorganic gas as the blowing agent or the mixed gas and then releasing the foamable resin particles out of the vessel while continuously maintaining the internal pressure of the vessel at a predetermined level.
- the resulting prefoamed particles can be obtained at a still greater expansion ratio with small variations.
- the inorganic gas contains oxygen, the oxidative deterioration of the resin particles and hence of the resulting prefoamed resin particles can be minimized.
- the melting point of the above resin is the temperature corresponding to the peak of an endothermic peak (inherent peak) on a DSC curve which is obtained when about 6 mg of its sample are heated at the rate of 10.C./min to 220° C, cooled at the cooling rate of 10° C./min to about 50° C. and again heated at the rate of 10° C./min to 220° C. on a differential scanning calorimeter.
- its melting completion temperature means the temperature given when the endothermic peak (inherent peak) on a second DSC curve obtained by a similar measurement to the above measurement returns to the position of the base line.
- the softening temperature of resin particles means the softening temperature as determined under the load of 4.6 kg/cm 2 in accordance with the method prescribed under ASTM-D-648.
- Each of the water-soluble inorganic substances shown in Table 1 was separately added in the corresponding amount, also shown in Table 1, per 100 parts by weight of an uncrosslinked ethylene-propylene random copolymer resin (ethylene content: 2.3 wt.%, melting point: 146.5° C., melting completion temperature: 165° C.), followed by melting and kneading in an extruder. After the resultant mass was extruded in the form of strands through a die fitted in a free end of the extruder and was then quenched in water, the strands were chopped so that they were pelletized into a pellet-like configuration (length of resin particles: 2.4 mm, diameter at cross-section of resin particles: 1.1 mm).
- Samples of prefoamed particles were produced following the procedures of Example 1-5 except that the starting resin particles in Examples 1-5 were changed to uncrosslinked propylene-butene random copolymer resin particles (butene content: 6 wt.%, melting point: 150° C., melting completion temperature: 163° C.) in Example 6 and to uncrosslinked linear low-density polyethylene-butene copolymer resin particles (butene content: 4.1 wt.%, melting point: 121° C, melting completion temperature: 135° C.) in Example 7.
- uncrosslinked propylene-butene random copolymer resin particles butene content: 6 wt.%, melting point: 150° C., melting completion temperature: 163° C.
- uncrosslinked linear low-density polyethylene-butene copolymer resin particles butene content: 4.1 wt.%, melting point: 121° C, melting completion temperature: 135° C.
- Example 7 The average bulk expansion ratio of each of the resultant samples of prefoamed particles and the maximum and minimum values of its bulk expansion ratio are also given in Table 1.
- Each of the water-soluble inorganic substances shown in Table 1 was separately added in the corresponding amount, also shown in the same table, per 100 parts by weight of an uncrosslinked ethylene-propylene random copolymer resin (ethylene content: 2.3 wt.%, melting point: 146.5° C., melting completion temperature: 165° C.), followed by melting and kneading in an extruder. After the resultant mass was extruded in the form of strands through a die fitted in a free end of the extruder and was then quenched in water, the strands were chopped so that they were pelletized into a pellet-like configuration (length of resin particles: 2.4 mm, diameter at cross-section of resin particles: 1.1 mm).
- the blowing agent carbon dioxide
- the vessel was opened at one end thereof under a back pressure applied with carbon dioxide so that the resin particles and water were released under the atmospheric pressure to allow the resin particles to undergo foaming.
- the average bulk expansion ratio of each of the resultant samples of prefoamed particles and the maximum and minimum values of its bulk expansion ratio are also given in Table 1.
- a propylene-ethylene random copolymer resin (ethylene content: 2.3 wt.%, melting completion temperature: 165° C.) was added with borax (Na 2 B 4 O 7 ⁇ 10H 2 O, average particle size: 50 ⁇ m) in a proportion to give 0.2 wt.% in an extruder, followed by melting and kneading.
- the resulting mass was extruded in the form of strands through a die fitted in a free end of the extruder and was then quenched in water.
- the strands were chopped into pellet-like particles (length of resin particles: 2.4 mm, diameter at cross-section of resin particles: 1.1 mm).
- the dispersion was heated to the second-stage holding temperature shown in the same table. While applying a back pressure with the mixed gas and maintaining the internal temperature and pressure of the vessel at the same levels, the vessel was opened at one end thereof so that the resin particles and water were released under the atmospheric pressure to allow the resin particles to undergo foaming.
- the average bulk expansion ratio of the resultant prefoamed particles and the maximum and minimum values of their bulk expansion ratio are also given in Table 2.
- Foaming was conducted in a similar manner to Example 10 except that the internal pressure of the vessel was maintained at 10 kg/cm 2 ⁇ G during foaming. The results are shown in Table 2.
- prefoamed particles were obtained under the conditions given in Table 2 by using resin particles which have been obtained in a similar manner to Examples 10-13 except for the use of a propylene-butene random copolymer resin (butene content: 6.0 wt.%, melting completion temperature: 163° C.) in place of the propylene-ethylene random copolymer resin.
- the average bulk expansion ratio of each of the resultant samples of prefoamed particles and the maximum d minimum values of its bulk expansion ratio are also given in Table 2.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Prefoamed synthetic resin particles are produced by dispersing foamable resin particles in a dispersing medium within a closed vessel, said foamable resin particles containing a water-soluble inorganic substance and a blowing agent therein, and then releasing the foamable resin particles and the medium into an atmosphere of a pressure lower than that inside the vessel, whereby the thus-released foamable resin particles are allowed to undergo foaming.
Description
a. Field of the Invention:
The present invention relates to a production method of prefoamed synthetic resin particles.
b. Description of the Related Art:
A process has conventionally been known, in which resin particles with a volatile blowing agent contained therein is dispersed in a dispersing medium such as water within a closed vessel, the resulting dispersion is heated to a temperature at least equal to the softening temperature of the resin particles with the internal pressure of the vessel being held at least equal to the vapor pressure of the blowing agent, thereby impregnating the resin particles with the blowing agent, and the vessel is opened at one end thereof to release the thus-impregnated resin particles and the dispersing medium into an atmosphere having a pressure lower than that inside the vessel, whereby the resin particles are allowed to undergo foaming. Exemplary volatile blowing agents useful in the practice of the above process primarily include hydrocarbons such as propane, butane and pentane; and halogenated hydrocarbons such as trichlorofluoromethane and dichloro-difluoromethane. Under the current circumstances, many of compounds employed as these volatile blowing agents however involve problems such as toxicity, inflammability and/or the like or the problem of ozonosphere destruction like flons or, even if rather free of serious problems from the standpoint of hazards or environmental destruction, the problem that the price is too high to permit commercial use. Further, a volatile blowing agent induces swelling of resin particles, thereby restricting the appropriate foaming temperature range upon foaming. As a result, the foaming temperature gives greater influence to the expansion ratio, leading to the problem that control of the expansion ratio becomes difficult.
A great deal of research has been made with a view toward overcoming these problems. The present inventors has also proceeded with an extensive investigation to solve such problems. The present inventors' investigation has already led to the proposal of processes for obtaining prefoamed synthetic resin particles by using a blowing agent of the inorganic gas type whose use as a blowing agent had never been thought of (for example, Japanese Patent Publication No. 61227/1987, Japanese Patent Application Laid-Open No. 2741/1986, Japanese Patent Application Laid-Open No. 4738/1986, etc.). The use of a blowing agent of the inorganic gas type however involves the problem that it hardly permits high-temperature foaming and hence the production of a foamed product having a high expansion ratio, because the blowing agent has poor impregnation property into resin particles and, moreover, secondary crystallization of the resin particles can be scarcely promoted. A blowing agent of the inorganic gas type is also accompanied by the problem that the reduction of expansion ratio becomes more conspicuous along the passage of time from the initiation of foaming, for example, an expansion ratio of about 20-30 times in the beginning of a foaming operation may decrease to an expansion ratio of about 10 times near the end of the foaming operation, resulting in substantial variations in expansion ratio.
The present inventors have proceeded with a further extensive investigation to overcome the above problems. As a result, the present inventors have found a process which permits the provision of prefoamed particles of a high expansion ratio even when they are produced on an industrial scale by using a blowing agent of the inorganic gas type and which, when a conventional volatile blowing agent is used, allows to reduce the amount of the blowing agent to be employed and permits the provision of prefoamed particles of a high expansion ratio still more stably than the process disclosed in Japanese Patent Application Laid-Open No. 4738/1986, leading to the completion of the present invention.
In one aspect of the present invention, there is thus provided a method for the production of prefoamed synthetic resin particles, which comprises:
dispersing foamable resin particles in a dispersing medium within a closed vessel, said foamable resin particles containing a water-soluble inorganic substance and a blowing agent therein; and
releasing the foamable resin particles and the medium into an atmosphere of a pressure lower than that inside the vessel, whereby the thus-released foamable resin particles are allowed to undergo foaming.
The present invention has numerous advantages. Since the foamable resin particles containing the water-soluble inorganic substance and the blowing agent are caused to undergo foaming in the process of the present invention, prefoamed particles of a high expansion ratio can be obtained easily even when a blowing agent of the inorganic gas type is used. When a volatile blowing agent is used, the process of the present invention makes it possible to reduce the amount of the volatile blowing agent to be used compared to the conventional processes which also make use of a similar volatile blowing agent and hence to permit the production of prefoamed particles of a high expansion ratio even when the volatile blowing agent is used in a small amount.
An inorganic gas can be used as the blowing agent. In this case, upon releasing the foamable resin particles into the atmosphere having the pressure lower than that inside the vessel and allowing them to undergo foaming, the same inorganic gas as the blowing agent or a mixed gas of the same inorganic gas as the blowing agent and another inorganic gas may be fed into the vessel to apply a back pressure so that the foaming can be conducted while maintaining the internal pressure of the vessel at a level at least equal to the prefoaming partial pressure of the blowing agent inside the vessel. This makes it possible to minimize variations of expansion ratio despite of the use of the blowing agent of the inorganic gas type. As a result, it is possible to avoid the problem that prefoamed particles obtained near the end of a foaming operation may differ significantly in expansion ratio from those obtained shortly after the initiation of the foaming operation immediately, thereby making it possible to produce excellent prefoamed particles throughout the foaming operation. When the resin particles are held at their foaming temperature for a while after the same inorganic gas as the blowing agent or the mixed gas of the same inorganic gas as the blowing agent and another inorganic gas has been fed into the vessel in the above process, the prefoamed particles can be obtained with a still greater expansion ratio. Moreover, the oxidative deterioration of the resin particles and hence the prefoamed resin particles can be minimized even when an oxygen-bearing inorganic gas is used as the inorganic gas.
The above and other objects, features and advantages of the present invention will become apparent from the following description and the appended claims, taken in conjunction with the accompanying drawings, in which:
FIG. 1 is a diagram showing a DSC curve of prefoamed particles containing secondary crystals therein; and
FIG. 2 is a diagram showing a DSC curve of prefoamed particles containing no secondary crystals therein.
Exemplary resin particles usable in the present invention include particles of polypropylene resins such as propylene homopolymer, propylene-ethylene random copolymers, propylene-ethylene block copolymers, propylene-butene random copolymers, propylene-ethylene-butene random copolymers, etc.; and particles of polyethylene resins such as high-density polyethylene, low-density polyethylene, linear low-density polyethylenes, etc. which are copolymers of ethylene with small amounts of α-olefins (carbon numbers: 4, 6, 8, etc.). Of these, polypropylene resins--such as propylene-ethylene random copolymers, propylene-butene random copolymers and propylene-ethylene-butene random copolymers--and linear low-density polyethylenes are preferred. Although these resins may be crosslinked, uncrosslinked resins are particularly preferred.
As resin particles, those containing a water-soluble inorganic substance are used in the present invention. Preferably, the water-soluble inorganic substance has a solubility of at least 1 g per 100 g of water of 40.C, with 5 g or higher being especially preferred. Illustrative of the water-soluble inorganic substance include borax, nickel sulfate, manganese sulfate, sodium chloride, magnesium chloride, calcium chloride, etc. Among these, borax is preferred. These inorganic substances can be used either singly or in combination. Each inorganic substance can be incorporated in resin particles by kneading it in a molten resin, extruding the resultant mass into strands, quenching the strands and then pelletizing the quenched strands. The inorganic substance is usually added in the form of powder, but not particular limitation is imposed on its average particle size. It is however generally preferred to use a water-soluble inorganic substance having an average particle size of 0.1-150μm, notably 1-100 μm. It is preferable to add one or more of these water-soluble inorganic substances in a total amount such that their total content in the resin particles ranges from 0.01 wt.% to 2 wt.%, especially from 0.02 wt.% to 1 wt.%. Addition of one or more of such inorganic substances in a large excess is not preferred because the resulting prefoamed particles will be prone to shrinkage and will thus not be preferable from the viewpoint of moldability. On the other hand, addition of one or more of the above inorganic substances in an unduly small amount will not be able to bring about the advantages of the present invention The preferable average particle size of the resin particles containing such inorganic substance or substances is generally 0.3-5 mm with 0.5-3 mm being especially preferred.
In the present invention, the step in which the resin particles are impregnated with the blowing agent may be either before or after the step in which the resin particles are dispersed in the dispersing medium within the closed vessel. In general, the impregnation of the resin particles is however carried out in the course of the step in which the resin particles are dispersed in the dispersing medium and is heated to their foaming temperature. In this case, the resin particles can be impregnated with the blowing agent, after once dissolving or dispersing the blowing agent in the dispersing medium. Namely, the resin particles can be impregnated, for example, by charging the resin particles, the blowing agent and the dispersing medium in a closed vessel and then heating and pressurizing them under stirring.
Blowing agents useful in the present invention include volatile blowing agents such as propane, butane, pentane, hexane, cyclobutane, cyclohexane, trichlorofluoromethane dichlorodifluoromethane monochlorodifluoromethane, 1-chloro-1,1-difluoroethane, 1,1,1,2-tetrachloroethane 1,1-dichloro-2,2,2-trifluoroethane, 1,1,1-difluoroethane and 1-chloro-1,2,2,2-tretrafluoroethane; and blowing agents of the inorganic gas type such as nitrogen, carbon dioxide, argon, air or the like. Among these, nitrogen, carbon dioxide and air are particularly preferred. When these blowing agents of the inorganic gas type are used, it is preferable to feed them to raise the internal pressure of the vessel to 20-50 kg/cm2 ·G.
Any dispersing medium can be used to disperse the resin particles as long as it does not dissolve the resin particles. Examples of the dispersing medium include water, ethylene glycol, glycerin, methanol, ethanol and the like. Water is usually employed.
Upon dispersing the foamable resin particles in the dispersing medium and then heating the resin particles to the foaming temperature, a fusion-bonding preventive can be used to prevent fusion-bonding of the resin particles. Any fusion-bonding preventive can be used regardless of whether it is inorganic or organic, so long as it is not dissolved in a dispersing medium such as water and is not molten under heat. Inorganic fusion-bonding preventives are generally preferred. Illustrative inorganic fusion-bonding preventives include aluminum oxide, titanium oxide, aluminum hydroxide, basic magnesium carbonate, basic zinc carbonate, calcium carbonate, tricalcium phosphate, and magnesium pyrophosphate. It is preferred to add one or more of these fusion-bonding preventives in combination with an emulsifier. Illustrative of the emulsifier include anionic surfactants such as sodium dodecylbenzenesulfonate and sodium oleate. As the above fusion-bonding preventive, those having an average particle size of 0.001-100 μm, especially 0.001-30 μm are preferred. Usually, the fusion-bonding preventive can be added preferably in an amount of 0.01-10 parts by weight per 100 parts by weight of the resin particles. Preferably, the emulsifier can be added generally in an amount of 0.001-5 parts by weight per 100 parts by weight of the resin particles.
In the process of the present invention, the inclusion of secondary crystals in the foamable resin particles is preferred. Prefoamed particles which have been obtained from foamable resin particles containing these secondary crystals have excellent moldability. The inclusion of secondary crystals in foamable resin particles is advantageous especially when the resin particles are made of a uncrosslinked polypropylene resin such as a propylene-ethylene random copolymer or an uncrosslinked linear low-density polyethylene resin. The existence of secondary crystals can be determined by whether or not a high-temperature peak on a side higher in temperature than an inherent peak attributed to endotherm upon so-called melting of the resin appears on a DSC curve obtained by differential scanning calorimetry of the resulting prefoamed particles. The inherent peak and high-temperature peak can each be determined by performing differential scanning calorimetry of the same sample twice. In this method, 1-10 mg of a sample (resin) is heated first to 220° C. at 10° C./min by a differential scanning calorimeter to obtain a first DSC curve. The sample is next cooled down from 220° C. to about 40° C. at a rate of 10° C./min and is again heated to 220° C. at 10° C./min, thereby obtaining a second DSC curve. By comparing the two DSC curves obtained as described above, the inherent peak and the high-temperature peak can be distinguished from each other. Since the inherent peak is an endothermic peak caused by so-called melting of the resin, it appears on both the first DSC curve and the second DSC curve. The highest temperature of the inherent peak may vary somewhat between the first measurement and the second measurement in some instances. The difference is however smaller than 5° C, usually not greater than 2° C. On the other hand, the high-temperature peak indicates an endothermic peak which appears on a side higher in temperature than the inherent peak on the first DSC curve. The existence of secondary crystals can be confirmed by the appearance of the high-temperature peak. When no substantial high-temperature peak appears, it is judged that no secondary crystals exist. With respect to the two DSC curves, the greater the difference between the highest temperature of the inherent peak appearing on the second DSC curve and that of the high-temperature peak appearing on the first DSC curve, the more desirable. The preferable temperature difference therebetween is at least 5° C. with 10° C. or greater being particularly preferred.
FIGS. 1 and 2 show DSC curves obtained by differential scanning calorimetry of prefoamed particles. FIG. 1 corresponds to prefoamed particles containing secondary crystals and FIG. 2 to prefoamed particles free of secondary crystals. In FIGS. 1 and 2, Curves 1 and 2 are DSC curves obtained by the first measurement, while Curves 1' and 2' are DSC curves obtained by the second measurement. As is shown in FIG. 1, on Curve 1 obtained by the first measurement, a high-temperature peak A which is not seen on Curve 1' obtained by the second measurement has appeared in addition to Inherent Peak B (Inherent Peak B' only appears on Curve 1' obtained by the second measurement). The existence of secondary crystals is confirmed by the appearance of the High-Temperature Peak A. In the case of prefoamed particles containing no secondary crystals on the other hand, as illustrated in FIG. 2, Inherent Peaks b, b' on Curves 2, 2' respectively but no high-temperature peaks appear. This makes it possible to confirm non-existence of secondary crystals. Particles in which existence of secondary crystals is not recognized like the prefoamed particles shown in FIG. 2 are obtained when the particles are allowed to undergo foaming at a temperature equal to or higher than their melting completion temperature without being subjected to heat treatment at a secondary crystallization promoting temperature (from the melting point to the melting completion temperature) for any sufficient time. When blowing agent of the inorganic gas type is used, prefoamed particles containing secondary crystals as shown by Curve 1 can be produced, for example, by a process as will be described next. In the case of a uncrosslinked polypropylene resin, such prefoamed particles can be obtained generally by holding resin particles at a temperature at least equal to (their melting point minus 20° C.) or so but lower than their melting completion temperature for a sufficient time, usually for 5-90 minutes, preferably for 15-60 minutes in a pressure vessel without raising the temperature of the resin particles to their melting completion temperature or higher. In the case of an uncrosslinked linear low-density polyethylene on the other hand, it is usually necessary to hold resin particles at a temperature at least equal to (their melting point minus 15° C.) or so but lower than their melting completion temperature for a sufficient time, generally for 5-90 minutes, preferably for 5-30 minutes in a pressure vessel without raising the temperature of the resin particles to their melting completion temperature or higher. Although the resin particles used in the above heating step may be foamable resin particles in which a blowing agent has already been incorporated, resin particles may be impregnated with the blowing agent concurrently with their heating in the heating step. In the case of resin particles in which secondary crystals have already been formed by heating and holding starting resin particles at such a temperature, prefoamed particles having good moldability can still be obtained even when the foaming temperature upon releasing the thus-heated foamable resin particles into an atmosphere having a pressure lower than that inside the vessel to allow them to undergo foaming (i.e., the temperature at the time of releasing) is equal to or higher than their melting completion temperature, so long as the foaming temperature is a temperature not higher than the high-temperature peak described above.
To facilitate control of the temperature, it is desirable to carry out the above heating and holding step as a plurality of sub-steps at different temperatures. In this case, the holding temperature in each sub-step is controlled higher than that in the preceding sub-step It is desirable to set the holding temperature of the last sub-step equal to the foaming temperature. Upon conducting the heating and holding step in a plurality of sub-steps as described above, resin particles can be impregnated with a blowing agent in the course of their heating in the heating step. In this case, the impregnation of the resin particles with the blowing agent can be effected after the resin particles have been heated to the final holding temperature (foaming temperature).
In the process of the present invention, the foaming temperature at which the foamable resin particles and the dispersing medium are released into an atmosphere having a pressure lower than that inside the vessel to allow the foamable resin particles to undergo foaming is a least equal to the softening temperature
t of the foamable resin particles. A temperature around the melting point is however particularly preferred. The preferred foaming temperature range varies depending on the kind of the resin. In the case of an uncrosslinked polypropylene resin for example, a temperature range at least equal to (the melting point minus 5.C.) but not higher than (the melting point plus 15° C.), especially a temperature range at least equal to (the melting point minus 3° C.) but not higher than (the melting point plus 10° C.) is preferred. In the case of a polyethylene resin, a temperature range at least equal to (the melting point minus 10° C.) but not higher than (the melting point plus 5° C.) is preferred. Further, the heating rate upon heating the resin particles to their foaming temperature is preferably 114 10° C./min, with 2-5° C./min being especially preferred. Upon releasing the foamable resin particles and the dispersing medium from the vessel, the pressure of the atmosphere may be any pressure lower than that inside the vessel but is the atmospheric pressure in general.
It is necessary to maintain the foamable resin particles under a pressure that prevents their foaming inside the vessel, generally at an elevated pressure of 5 kg/cm2 ·G or higher. In some conventional processes in which foamable resin particles are released into an atmosphere having a pressure lower than that inside the vessel to allow them to undergo foaming, it is attempted to stabilize the expansion ratio by holding foamable resin particles at foaming temperature for a while and then releasing them from the vessel by applying a back pressure with nitrogen gas while maintaining the internal pressure of the vessel at a level equal to or higher than the vapor pressure of an associated blowing agent.
However, when a blowing agent of the inorganic gas type, typically carbon dioxide is used and foamable resin particles are released for their foaming into an atmosphere having a pressure lower than that inside the vessel while applying a back pressure with nitrogen gas alone as in the conventional foaming processes, the expansion ratio of the resulting prefoamed particles decreases considerably as time goes on from the initiation of the release. Use of a blowing agent of the inorganic gas type as a blowing agent therefore requires to conduct the foaming while applying a back pressure with the same inorganic gas as the inorganic gas employed as a blowing agent or with a mixed gas of the same inorganic gas and another inorganic gas. When the blowing agent is a mixed gas such as air, the same inorganic gas as the blowing agent, said same inorganic gas being employed to apply the back pressure, is only required to have the same principal components. When the blowing agent is air by way of example, it is possible to use air, nitrogen, an air/nitrogen mixed gas or the like as the same inorganic gas as the blowing agent. When carbon dioxide is employed as a blowing agent, it is preferable to use nitrogen, air, argon or the like as another inorganic gas different from the inorganic gas employed as the blowing agent. The mixing ratio of the same inorganic gas as the blowing agent to another inorganic gas may preferably range from 3:7 to 9.5:0.5 by weight. This mixed gas is supplied such that the internal pressure of the vessel is maintained at a level at least equal to the prefoaming partial pressure of the blowing agent of the inorganic gas type inside the vessel throughout the step in which the resin particles are released. If the internal pressure of the vessel during the foaming is lower than the partial pressure of the blowing agent of the inorganic gas type inside the vessel before the foaming, the expansion ratio of the resulting prefoamed particles gradually becomes smaller although this decrease of the expansion ratio varies depending on the level of the internal pressure of the vessel during the foaming. The preferred pressure range of a mixed gas to be fed to apply a back pressure is 10-50 kg/cm2 ·G when its mixing ratio falls within the range specified above.
When a blowing agent of the inorganic gas type is used, it is preferable to perform foaming by impregnating resin particles with the blowing agent within a vessel, feeding the same inorganic gas as the blowing agent or a mixed gas of the same inorganic gas and another inorganic gas different from the blowing agent, said former same inorganic gas or said another inorganic gas having a pressure at least equal to the partial pressure of the blowing agent in the vessel, into the vessel and once holding the thus-impregnated resin particles at their foaming temperature, and then releasing the resulting resin particles from the vessel while applying a back pressure as described above. The another inorganic gas as employed here is similar to the another inorganic gas employed in the above-described mixed gas and is different from the inorganic gas employed as the blowing agent. When the blowing agent is carbon dioxide, the term "another inorganic gas" means an inorganic gas other than carbon dioxide. In this process, it is desirable to feed the same inorganic gas as the blowing agent or the mixed gas of the same inorganic gas as the blowing agent and another inorganic gas immediately after raising the internal temperature of the vessel to the foaming temperature. The most desirable embodiment of this process comprises applying a predetermined back pressure immediately after the internal temperature of the vessel has been raised to the foaming temperature, maintaining resin particles for a while under the same conditions to promote further impregnation of the resin particles with the same inorganic gas as the blowing agent or the mixed gas and then releasing the foamable resin particles out of the vessel while continuously maintaining the internal pressure of the vessel at a predetermined level.
When resin particles are foamed as described above, the resulting prefoamed particles can be obtained at a still greater expansion ratio with small variations. In addition, even when the inorganic gas contains oxygen, the oxidative deterioration of the resin particles and hence of the resulting prefoamed resin particles can be minimized.
In this invention, the melting point of the above resin is the temperature corresponding to the peak of an endothermic peak (inherent peak) on a DSC curve which is obtained when about 6 mg of its sample are heated at the rate of 10.C./min to 220° C, cooled at the cooling rate of 10° C./min to about 50° C. and again heated at the rate of 10° C./min to 220° C. on a differential scanning calorimeter. On the other hand, its melting completion temperature means the temperature given when the endothermic peak (inherent peak) on a second DSC curve obtained by a similar measurement to the above measurement returns to the position of the base line. Further, the softening temperature of resin particles means the softening temperature as determined under the load of 4.6 kg/cm2 in accordance with the method prescribed under ASTM-D-648.
The present invention will hereinafter be described in further detail by the following examples.
Each of the water-soluble inorganic substances shown in Table 1 was separately added in the corresponding amount, also shown in Table 1, per 100 parts by weight of an uncrosslinked ethylene-propylene random copolymer resin (ethylene content: 2.3 wt.%, melting point: 146.5° C., melting completion temperature: 165° C.), followed by melting and kneading in an extruder. After the resultant mass was extruded in the form of strands through a die fitted in a free end of the extruder and was then quenched in water, the strands were chopped so that they were pelletized into a pellet-like configuration (length of resin particles: 2.4 mm, diameter at cross-section of resin particles: 1.1 mm). Those resin particles (100 kg) were added with 400 g of fine aluminum oxide powder and 220 l of water. Without raising the temperature of the resin particles to their melting completion temperature or higher, the resultant dispersion was heated to the first-stage holding temperature shown in Table 1 and held at that temperature, under stirring within a closed vessel (capacity: 400 l). The dispersion was then heated to the second-stage holding temperature shown in Table 1. Immediately after that the corresponding blowing agent also given in the same table was fed to raise the internal pressure of the vessel to the corresponding pressure indicated in the same table and the dispersion was thereafter held at the same temperature. While being maintained at the second-stage holding temperature, a back pressure was applied with nitrogen gas or air (which was chosen to be consistent with the blowing agent employed). While the internal pressure of the vessel was maintained at the level indicated in Table 1, the vessel was opened at one end thereof so that the resin particles and water were released under the atmospheric pressure to allow the resin particles to undergo foaming. The average bulk expansion ratio of each of the resultant samples of prefoamed particles and the maximum and minimum values of its bulk expansion ratio are also given in Table 1.
Following the procedures of Examples 1-5 except that the pelletization was conducted by separately adding the non-water-soluble inorganic substances shown in Table 1, foaming was carried out under the conditions given in Table 1 while using a similar ethylene-propylene random copolymer resin to that employed in the examples. The average bulk expansion ratio of each of the resultant samples of prefoamed particles and the maximum and minimum values of its bulk expansion ratio are also given in Table 1.
Samples of prefoamed particles were produced following the procedures of Example 1-5 except that the starting resin particles in Examples 1-5 were changed to uncrosslinked propylene-butene random copolymer resin particles (butene content: 6 wt.%, melting point: 150° C., melting completion temperature: 163° C.) in Example 6 and to uncrosslinked linear low-density polyethylene-butene copolymer resin particles (butene content: 4.1 wt.%, melting point: 121° C, melting completion temperature: 135° C.) in Example 7.
It is however to be noted that the second-stage holding was not effected in Example 7. The average bulk expansion ratio of each of the resultant samples of prefoamed particles and the maximum and minimum values of its bulk expansion ratio are also given in Table 1.
Following the procedures of Examples 6-7 except for the use of CaCO3 as an inorganic substance, foaming was carried out. The average bulk expansion ratio of each of the resultant samples of prefoamed particles and the maximum and minimum values of its bulk expansion ratio are also given in Table 1.
Each of the water-soluble inorganic substances shown in Table 1 was separately added in the corresponding amount, also shown in the same table, per 100 parts by weight of an uncrosslinked ethylene-propylene random copolymer resin (ethylene content: 2.3 wt.%, melting point: 146.5° C., melting completion temperature: 165° C.), followed by melting and kneading in an extruder. After the resultant mass was extruded in the form of strands through a die fitted in a free end of the extruder and was then quenched in water, the strands were chopped so that they were pelletized into a pellet-like configuration (length of resin particles: 2.4 mm, diameter at cross-section of resin particles: 1.1 mm). Those resin particles (100 kg) were added with 1.5 kg of fine particulate tricalcium phosphate, 40 g of sodium dodecylbenzenesulfonate, 220 l of water and 7.5 kg (in Example 8) or 7 kg (in Example 9) of solid carbon dioxide (dry ice) as a blowing agent. Without raising the temperature of the resin particles to their melting completion temperature or higher, the resultant dispersion was heated to the first-stage holding temperature shown in Table 1 and held at that temperature, under stirring within a closed vessel (capacity: 400 l). The dispersion was then heated to the second-stage holding temperature shown in Table 1. Immediately after that, the blowing agent (carbon dioxide) was fed further to raise the internal pressure of the vessel to the corresponding pressure indicated in the same table and the dispersion was thereafter held at the same temperature. While being maintained at the second-stage holding temperature, the vessel was opened at one end thereof under a back pressure applied with carbon dioxide so that the resin particles and water were released under the atmospheric pressure to allow the resin particles to undergo foaming. The average bulk expansion ratio of each of the resultant samples of prefoamed particles and the maximum and minimum values of its bulk expansion ratio are also given in Table 1.
TABLE 1
__________________________________________________________________________
Internal pressure
Inorganic substance of vessel right
First-stage
Second-stage
Solubility in
Amount
before feeding
holding holding
100 g of water
added
inorganic gas
Temperature
Time
Temperature
Time
Kind of 40° C.
(wt. part)
(kg/cm.sup.2 · G)
(°C.)
(min)
(°C.)
(min)
__________________________________________________________________________
Example
1 Borax (anhydrous)
≧20 g
0.3 6 150 15 155 15
2 Borax (decahydrate)
≧20 g
0.2 6 150 15 155 15
3 Aluminum sulfate
≧20 g
0.2 6 150 15 155 15
(octadecahydrate)
4 Nickel sulfate
≧20 g
0.2 6 150 15 155 15
(hexahydrate)
5 Sodium chloride
≧20 g
0.2 6 150 15 155 15
6 Borax (decahydrate)
≧20 g
0.4 6 152 15 157 15
7 Borax (decahydrate)
≧20 g
0.5 6 115 15 -- --
8 Borax (anhydrous)
≧20 g
0.2 .sup. 40.5.sup.1)
148 15 153 15
9 Borax (anhydrous)
≧20 g
0.2 36.sup.2)
147 15 152 15
Comp. Ex.
1 Aluminum hydroxide
0 g 0.3 6 150 15 155 15
2 Calcium carbonate
0.0015 g
0.2 6 150 15 155 15
3 Calcium carbonate
0.0015 g
0.4 6 152 15 157 15
4 Calcium carbonate
0.0015 g
0.5 6 115 15 -- --
__________________________________________________________________________
Blowing agent Blowing conditions
Prefoamed particles
Internal pressure
Internal Secondary
Average
of vessel after
pressure of
crystals
bulk Variations of
feeding inorganic
vessel during
in pre-
expansion
expansion ratio
gas foaming foamed
ratio Maximum
Minimum
Kind (kg/cm.sup.2 · G)
(kg/cm.sup.2 · G)
particles
(times) (times)
(times)
__________________________________________________________________________
Example
1 Air 50 47 Contained
22 23 20
2 Nitrogen
45 45 Contained
19 21 18
3 Air 45 42 Contained
23 24 22
4 Air 45 45 Contained
17 18 16
5 Air 45 45 Contained
15 16 14
6 Air 30 28 Contained
20 21 19
7 Air 45 43 Contained
13 14 13
8 CO.sub.2
45 42 Contained
54 55 53
9 CO.sub.2
36 36 Contained
31 31 29
Comp. Ex.
1 Air 50 47 Contained
12 13 11
2 Nitrogen
45 45 Contained
11 12 11
3 Air 30 28 Contained
7 8 7
4 Air 25 28 Contained
6 6 5
__________________________________________________________________________
.sup.1) Due to advance addition of 7.5 kg of dry ice.
.sup.2) Due to advance addition of 7.0 kg of dry ice.
In each example, a propylene-ethylene random copolymer resin (ethylene content: 2.3 wt.%, melting completion temperature: 165° C.) was added with borax (Na2 B4 O7 ·10H2 O, average particle size: 50 μm) in a proportion to give 0.2 wt.% in an extruder, followed by melting and kneading. The resulting mass was extruded in the form of strands through a die fitted in a free end of the extruder and was then quenched in water. The strands were chopped into pellet-like particles (length of resin particles: 2.4 mm, diameter at cross-section of resin particles: 1.1 mm). Those particles (100 kg) were added with 1 kg of tricalcium phosphate, 250 q of sodium dodecylbenzenesulfonate, 220 l of water and dry ice as a blowing agent in the corresponding amount shown in Table 2. Without raising the temperature of the particles to their melting completion temperature or higher, the resultant dispersion was heated to the first-stage holding temperature shown in the same table and held at that temperature, under stirring within a closed vessel (capacity: 400 l). Next, with a mixed gas obtained by adding the inorganic gas shown in Table 2 to 100 parts of carbon dioxide at the weight ratio given in the same table, the internal pressure of the vessel was elevated to the level shown in the same table. At the same time, the dispersion was heated to the second-stage holding temperature shown in the same table. While applying a back pressure with the mixed gas and maintaining the internal temperature and pressure of the vessel at the same levels, the vessel was opened at one end thereof so that the resin particles and water were released under the atmospheric pressure to allow the resin particles to undergo foaming. The average bulk expansion ratio of the resultant prefoamed particles and the maximum and minimum values of their bulk expansion ratio are also given in Table 2.
In a similar manner to Examples 10 and 11 except that pelletization was conducted without addition of borax, foaming was carried out using a similar propylene-ethylene random copolymer to that employed in Examples 10 and 11. The average bulk expansion ratio of each of the resultant samples of prefoamed particles and the maximum and minimum values of its bulk expansion ratio are also given in Table 2.
Foaming was conducted in a similar manner to Example 10 except that the internal pressure of the vessel was maintained at 10 kg/cm2 ·G during foaming. The results are shown in Table 2.
In the procedures of Examples 12 and 13, the back pressure was applied using nitrogen alone instead of the mixed gas of carbon dioxide and air. The internal pressure of the vessel after the feeding of nitrogen Was set at the same level as in Examples 12 and 13. The average bulk expansion ratio of the resultant prefoamed particles and the maximum and minimum values of their bulk expansion ratio are also given in Table 2.
In each example, prefoamed particles were obtained under the conditions given in Table 2 by using resin particles which have been obtained in a similar manner to Examples 10-13 except for the use of a propylene-butene random copolymer resin (butene content: 6.0 wt.%, melting completion temperature: 163° C.) in place of the propylene-ethylene random copolymer resin. The average bulk expansion ratio of each of the resultant samples of prefoamed particles and the maximum d minimum values of its bulk expansion ratio are also given in Table 2.
TABLE 2
__________________________________________________________________________
Vapor pressure
Amount of Heating temperature conditions
of carbon
blowing First-stage
Second-stage
dioxide in
agent (dry holding holding vessel right
Inorganic gas
ice) added Temp.
Time Temp.
Time before feeding
in mixed gas
(kg) (°C.)
(min)
(°C.)
(min)
mixed gas
Kind Proportion
__________________________________________________________________________
Example
10 2 148 15 153 15 14 Nitrogen
70
11 2 148 15 153 15 14 Nitrogen
70
12 4 148 15 153 15 21 Air 60
13 7 147 15 152 15 33 Air 30
14 4 149 15 154 15 21 Air 60
15 7 148 15 153 15 33 Nitrogen
30
Comp. Ex.
5 2 148 15 153 15 14 Nitrogen
70
6 2 148 15 153 15 14 Nitrogen
70
7 2 148 15 153 15 14 Nitrogen
70
8 4 148 15 153 15 21 -- --
9 7 147 15 152 15 33 -- --
__________________________________________________________________________
Internal
pressure Secondary
Prefoamed particles
of vessel crystals
Average bulk
Variations
during in expansion
of expansion ratio
foaming prefoamed
ratio Maximum
Minimum
(kg/cm.sup.2 · G)
Feeding time of mixed gas
particles
(times)
(times)
(times)
__________________________________________________________________________
Example
10 35 Immediately before foaming
Contained
15 18 14
11 35 Right after the initiation
Contained
17 18 16
of second-stage holding
12 40 Right after the initiation
Contained
22 23 21
of second-stage holding
13 45 Right after the initiation
Contained
32 33 31
of second-stage holding
14 40 Right after the initiation
Contained
23 24 22
of second-stage holding
15 45 Right after the initiation
Contained
33 34 32
of second-stage holding
Comp. Ex.
5 35 Immediately before foaming
Contained
8 9 7
6 35 Right after the initiation
Contained
10 11 9
of second-stage holding
7 10 Right after the initiation
Contained
5 7 2
of second-stage holding
8 40 Right after the initiation
Contained
8 11 4
of second-stage holding*)
9 45 Right after the initiation
Contained
24 32 15
of second-stage holding*)
__________________________________________________________________________
*)Feeding time of nitrogen gas
Claims (17)
1. A method for the production of prefoamed synthetic resin particles, which comprises:
dispersing foamable resin particles in a dispersing medium with a closed vessel, said foamable resin particles containing a water-soluble inorganic salt in a total amount of 0.01 to 2.0 wt.% based on the resin particles and a blowing agent therein;
heating the foamable resin particles to a temperature at least equal to the softening point thereof in the dispersing medium within the closed vessel; and
releasing the foamable resin particles and the medium into an atmosphere of a pressure lower than that inside the vessel, whereby the thus-released foamable resin particles are allowed to undergo foaming.
2. A method for the production of prefoamed synthetic resin particles, which comprises:
releasing foamable resin particles--which have been obtained by dispersing resin particles, with a water-soluble inorganic salt contained therein in a total amount of 0.01 to 2.0 wt.% based on the resin particles, in a dispersing medium within a closed vessel and then impregnating the resin particles with a blowing agent--together with the dispersing medium at a temperature at least equal to the softening point thereof into an atmosphere of a pressure lower than that inside the vessel, whereby the thus-released foamable resin particles are allowed to undergo foaming.
3. A method for the production of prefoamed synthetic resin particles, which comprises:
dispersing foamable resin particles having been obtained by impregnating with a blowing agent of the inorganic gas type uncrosslinked polypropylene resin particles containing a water-soluble inorganic salt therein in a total amount of 0.01 to 2.0 wt.% based on the resin particles;
holding the foamable resin particles for 5-90 minutes at a temperature at least equal to (the melting point of the foamable resin particles minus 20° C.) but lower than the melting completion temperature thereof without raising the temperature of the foamable resin particles to the melting completion temperature thereof or higher in the course of the heating thereof; and
releasing the foamable resin particles and the medium at a temperature at least equal to (the melting point of the foamable resin particles minus 5° C.) but not higher than (the melting point of the foamable resin particles plus 15° C.) into an atmosphere of a pressure lower than that inside the vessel, whereby the thus-released foamable resin particles are allowed to undergo foaming.
4. A method for the production of prefoamed synthetic resin particles, which comprises:
dispersing uncrosslinked polypropylene resin particles in a dispersing medium within a closed vessel, said uncrosslinked polypropylene resin particles containing a water-soluble inorganic salt therein in a total amount of 0.01 to 2.0 wt.% based on the resin particles;
holding the uncrosslinked polypropylene resin particles for 5-90 minutes at a temperature at least equal to (the melting point of the foamable resin particles minus 20° C.) but lower than the melting completion temperature thereof without raising the temperature of the uncrosslinked polypropylene resin particles to the melting completion temperature thereof or higher in the course of the heating thereof; and
feeding a blowing agent of the inorganic gas type into a closed vessel;
impregnating the uncrosslinked polypropylene resin particles with a blowing agent of the inorganic gas type at a temperature at least equal to (the melting point of the resin particles minus 5° C.) but not higher than (the melting point of the resin particles plus 15° C.), thereby forming foamable resin particles; and releasing the foamable resin particles and the medium at the same temperature into an atmosphere of a pressure lower than that inside the vessel, whereby the thus-released foamable resin particles are allowed to undergo foaming.
5. A method for the production of prefoamed synthetic resin particles, which comprises:
dispersing foamable resin particles in a dispersing medium within a closed vessel, said foamable resin particles having been obtained by impregnating with a blowing agent of the inorganic gas type uncrosslinked linear low-density polyethylene resin particles containing a water-soluble inorganic salt therein in a total amount of 0.01 to 2.0 wt.% based on the resin particles;
holding the foamable resin particles for 5-90 minutes at a temperature at least equal to (the melting point of the foamable resin particles minus 15° C.) but lower than the melting completion temperature thereof without raising the temperature of the foamable resin particles to the melting completion temperature thereof or higher in the course of the heating thereof; and
releasing the foamable resin particles and the medium at a temperature at least equal to (the melting point of the foamable resin particles minus 10° C.) but not higher than (the melting point of the foamable resin particles plus 5° C.) into an atmosphere of a pressure lower than that inside the vessel, whereby the thus-released foamable resin particles are allowed to undergo foaming.
6. A method for the production of prefoamed synthetic resin particles, which comprises:
dispersing uncrosslinked linear low-density
polyethylene resin particles in a dispersing medium within a closed vessel, said uncrosslinked polyethylene resin particles containing a water-soluble inorganic salt therein in a total amount of 0.01 to 2.0 wt.% based on the resin particles;
holding the uncrosslinked low-density polyethylene resin particles for 5-90 minutes at a temperature at least equal to (the melting point of the uncrosslinked linear low-density polyethylene resin particles minus 15° C.) but lower than the melting completion temperature thereof without raising the temperature of the melting completion temperature thereof or higher in the course of the heating thereof;
feeding a blowing agent of the inorganic gas type into a closed vessel;
impregnating the uncrosslinked linear low-density polyethylene resin particles with a blowing agent of the inorganic gas type at a temperature at least equal to (the melting point of the uncrosslinked linear low density polyethylene resin particles minus 10° C.) but not higher than (the melting point of the uncrosslinked linear low-density polyethylene resin particles plus 5° C.), thereby forming foamable resin particles; and
releasing the foamable resin particles and the dispersing medium into an atmosphere of a pressure lower than that inside the vessel, whereby the resin particles are allowed to undergo foaming.
7. A method for the production of prefoamed synthetic resin particles, which comprises:
dispersing resin particles, which contain a water-soluble inorganic salt therein in a total amount of 0.01 to 2.0 wt.% based on the resin particles, in the presence of a blowing agent of the inorganic gas type in a dispersing medium within a closed vessel and then heating the resin particles to a least a temperature at which the resin particles are softened, whereby the resin particles are impregnated with the blowing agent of the inorganic gas type; and
releasing the thus-impregnated foamable resin particles and the dispersing medium into an atmosphere of a pressure lower than that inside the vessel while applying a back pressure with the same inorganic gas as the blowing agent or a mixed gas of the same inorganic gas as the blowing agent and another inorganic gas different from the blowing agent such that the internal pressure of the vessel is held at a pressure at least equal to the partial pressure of the blowing agent of the inorganic gas type within the vessel, whereby the thus-released resin particles are allowed to undergo foaming.
8. A method for the production of prefoamed synthetic resin particles, which comprises:
dispersing resin particles, which contain a water-soluble inorganic salt therein in a total amount of 0.01 to 2.0 wt.% based on the resin particles, in the presence of a blowing agent of the inorganic gas type in a dispersing medium within a closed vessel and then heating the resin particles to a least a temperature at which the resin particles are softened, whereby the resin particles are impregnated with the blowing agent of the inorganic gas type;
feeding the same inorganic gas as the blowing agent of a mixed gas of the same inorganic gas as the blowing agent and another inorganic gas different from the blowing agent, said former same inorganic gas or mixed gas having a partial pressure at least equal to the partial pressure of the blowing agent of the inorganic gas type in the vessel, into the vessel and holding the thus-impregnated resin particles at a foaming temperature thereof; and
releasing the thus-impregnated foamable resin particles and the dispersing medium into an atmosphere of a pressure lower than that inside the vessel while applying a back pressure with the same inorganic gas as the blowing agent or a mixed gas of the same inorganic gas as the blowing agent and another inorganic gas different from the blowing agent such that the internal pressure of the vessel is held at a pressure at least equal to the partial pressure of the blowing agent of the inorganic gas type within the vessel, whereby the thus-released resin particles are allowed to undergo foaming.
9. A method of claim 1 or 2, wherein the blowing agent is a volatile blowing agent.
10. A method of claim 1 or 2, wherein the blowing agent is of the inorganic gas type.
11. A method of claim 7 or 8, wherein the thus-impregnated resin particles and the dispersing medium are released while applying a back pressure with a mixed gas of the same inorganic gas as the blowing agent and another inorganic gas different from the blowing agent at a weight ratio of from 3:7 to 9.5:0.5.
12. The method of any one of claims 1-8, wherein the water-soluble inorganic salt is borax.
13. The method of any one of claims 1-8, wherein the water-soluble inorganic salt is contained in a proportion of 0.02-1 wt.% based on the resin particles.
14. The method of any one of claims 1-8, wherein the water-soluble inorganic salt has an average particle size of 0.1-150 μm.
15. The method of any one of claims 1-8, wherein the solubility of the water-soluble inorganic salt in 100 g of water of 40° C. is at least 5 g.
16. The method of any one of claims 1-8 wherein the solubility of the water-soluble inorganic salt in 100 g of water of 40° C. is at least 1 g.
17. The method of any one of claims 1-8 wherein the water-soluble inorganic salt is selected from the group consisting of borax, nickel sulfate, manganese sulfate, sodium chloride, magnesium chloride and calcium chloride.
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1-307869 | 1989-11-24 | ||
| JP1-307868 | 1989-11-24 | ||
| JP30786989 | 1989-11-24 | ||
| JP1307868A JP2874772B2 (en) | 1989-11-24 | 1989-11-24 | Method for producing expanded polymer particles |
| JP2-202238 | 1990-07-30 | ||
| JP20223890A JP2826769B2 (en) | 1989-11-24 | 1990-07-30 | Method for producing expanded polymer particles |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US5122545A true US5122545A (en) | 1992-06-16 |
Family
ID=27328066
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/617,578 Expired - Lifetime US5122545A (en) | 1989-11-24 | 1990-11-26 | Production method of prefoamed synthetic resin particles |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US5122545A (en) |
| EP (1) | EP0429091B1 (en) |
| KR (1) | KR0157621B1 (en) |
| CA (1) | CA2030754C (en) |
| DE (1) | DE69022814T2 (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5380766A (en) * | 1993-06-14 | 1995-01-10 | Huels Aktiengesellschaft | Process for the preparation of prefoamed polyolefin particles |
| US5480599A (en) * | 1992-04-09 | 1996-01-02 | Huels Aktiengesellschaft | Method of manufacturing foam beads |
| US5836685A (en) * | 1996-04-02 | 1998-11-17 | Lambert, Sr.; Raymond E. | Method for continuously treating particulate material in a slurry in a high temperature and high pressure chamber employing intermittent feed |
| US6034144A (en) * | 1998-06-11 | 2000-03-07 | Jsp Corporation | Molded article of foamed and expanded beads of propylene resin |
| US6077875A (en) * | 1998-03-23 | 2000-06-20 | Jsp Corporation | Foamed and expanded beads of polypropylene resin for molding |
| US6133331A (en) * | 1996-12-13 | 2000-10-17 | Jsp Corporation | Expanded particles of polyolefin resin and process for preparing the same |
| US6313184B1 (en) | 1997-12-01 | 2001-11-06 | Jsp Corporation | Expanded polypropylene resin beads and a molded article |
| US6451419B1 (en) | 1996-08-12 | 2002-09-17 | Jsp Corporation | Shock absorbing material |
| US6547996B1 (en) | 1997-06-18 | 2003-04-15 | Jsp Corporation | Production apparatus of expansion-molded article, auxiliary member for transfer of foamed particles and production method of expansion-molded article |
| US20040108616A1 (en) * | 2002-04-26 | 2004-06-10 | Andreas Beckmann | Method for producing a foamable plastic |
| US6818161B2 (en) | 1997-04-01 | 2004-11-16 | Jsp Corporation | Molded body of thermoplastic resin having sound absorption characteristics |
| US8513317B2 (en) | 2007-12-11 | 2013-08-20 | Kaneka Corporation | Process for producing expanded polyolefin resin particles and expanded polyolefin resin particles |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19737002A1 (en) | 1997-08-26 | 1999-03-04 | Basf Ag | Process for the production of expanded polyolefin particles |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4226942A (en) * | 1978-08-15 | 1980-10-07 | Monsanto Company | Foamable resins process |
| US4303756A (en) * | 1978-10-16 | 1981-12-01 | Sekisui Kaseihin Kogyo Kabushiki Kaisha | Process for producing expandable thermoplastic resin beads |
| US4436840A (en) * | 1981-09-28 | 1984-03-13 | Japan Styrene Paper Corporation | Process for producing pre-foamed particles of polyolefin resin |
| US4602047A (en) * | 1983-08-26 | 1986-07-22 | Yuka Badische Co., Ltd. | Process for producing foamed particles of polyolefin resin |
| US4676939A (en) * | 1984-06-14 | 1987-06-30 | Japan Styrene Paper Corporation | Process for the production of expanded particles of a polypropylene resin |
| US4908393A (en) * | 1988-03-24 | 1990-03-13 | Mitsubishi Yuka Badische Co., Ltd. | Propylene resin foamed particles and foamed mold article |
| US4948817A (en) * | 1987-06-23 | 1990-08-14 | Japan Styrene Paper Corporation | Pre-foamed particles of uncrosslinked, linear low-density polyethylene and production method thereof |
| US5015667A (en) * | 1983-10-24 | 1991-05-14 | Japan Styrene Paper Corporation | Pre-foamed beads of polyethylene base resin |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1450057A (en) * | 1972-12-07 | 1976-09-22 | Fisons Ltd | Blowing agent compositions |
| IN139125B (en) * | 1973-04-25 | 1976-05-08 | Ishikawa T | |
| US4021380A (en) * | 1976-02-27 | 1977-05-03 | Mattel, Inc. | Expandable resin composition |
| AU559244B2 (en) * | 1982-05-13 | 1987-03-05 | Kanegafuchi Kagaku Kogyo K.K. | Expanded polyolefin particles |
| US4704239A (en) * | 1984-04-28 | 1987-11-03 | Japan Styrene Paper Corp. | Process for the production of expanded particles of a polymeric material |
| JPH082989B2 (en) * | 1987-05-11 | 1996-01-17 | 日本スチレンペ−パ−株式会社 | Pre-expansion method of polyolefin resin particles |
| JP2887291B2 (en) * | 1989-08-30 | 1999-04-26 | 株式会社ジェイエスピー | Method for producing expanded polyolefin resin particles |
-
1990
- 1990-11-23 CA CA002030754A patent/CA2030754C/en not_active Expired - Fee Related
- 1990-11-24 EP EP90122447A patent/EP0429091B1/en not_active Revoked
- 1990-11-24 DE DE69022814T patent/DE69022814T2/en not_active Revoked
- 1990-11-24 KR KR1019900019120A patent/KR0157621B1/en not_active IP Right Cessation
- 1990-11-26 US US07/617,578 patent/US5122545A/en not_active Expired - Lifetime
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4226942A (en) * | 1978-08-15 | 1980-10-07 | Monsanto Company | Foamable resins process |
| US4303756A (en) * | 1978-10-16 | 1981-12-01 | Sekisui Kaseihin Kogyo Kabushiki Kaisha | Process for producing expandable thermoplastic resin beads |
| US4436840A (en) * | 1981-09-28 | 1984-03-13 | Japan Styrene Paper Corporation | Process for producing pre-foamed particles of polyolefin resin |
| US4602047A (en) * | 1983-08-26 | 1986-07-22 | Yuka Badische Co., Ltd. | Process for producing foamed particles of polyolefin resin |
| US5015667A (en) * | 1983-10-24 | 1991-05-14 | Japan Styrene Paper Corporation | Pre-foamed beads of polyethylene base resin |
| US4676939A (en) * | 1984-06-14 | 1987-06-30 | Japan Styrene Paper Corporation | Process for the production of expanded particles of a polypropylene resin |
| US4948817A (en) * | 1987-06-23 | 1990-08-14 | Japan Styrene Paper Corporation | Pre-foamed particles of uncrosslinked, linear low-density polyethylene and production method thereof |
| US4908393A (en) * | 1988-03-24 | 1990-03-13 | Mitsubishi Yuka Badische Co., Ltd. | Propylene resin foamed particles and foamed mold article |
| US5032620A (en) * | 1988-03-24 | 1991-07-16 | Mitsubishi Yuka Badische Co., Ltd. | Propylene resin foamed particles and foamed mold article |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5480599A (en) * | 1992-04-09 | 1996-01-02 | Huels Aktiengesellschaft | Method of manufacturing foam beads |
| US5380766A (en) * | 1993-06-14 | 1995-01-10 | Huels Aktiengesellschaft | Process for the preparation of prefoamed polyolefin particles |
| US5836685A (en) * | 1996-04-02 | 1998-11-17 | Lambert, Sr.; Raymond E. | Method for continuously treating particulate material in a slurry in a high temperature and high pressure chamber employing intermittent feed |
| US6451419B1 (en) | 1996-08-12 | 2002-09-17 | Jsp Corporation | Shock absorbing material |
| US6133331A (en) * | 1996-12-13 | 2000-10-17 | Jsp Corporation | Expanded particles of polyolefin resin and process for preparing the same |
| US6818161B2 (en) | 1997-04-01 | 2004-11-16 | Jsp Corporation | Molded body of thermoplastic resin having sound absorption characteristics |
| US6547996B1 (en) | 1997-06-18 | 2003-04-15 | Jsp Corporation | Production apparatus of expansion-molded article, auxiliary member for transfer of foamed particles and production method of expansion-molded article |
| US6313184B1 (en) | 1997-12-01 | 2001-11-06 | Jsp Corporation | Expanded polypropylene resin beads and a molded article |
| US6077875A (en) * | 1998-03-23 | 2000-06-20 | Jsp Corporation | Foamed and expanded beads of polypropylene resin for molding |
| US6034144A (en) * | 1998-06-11 | 2000-03-07 | Jsp Corporation | Molded article of foamed and expanded beads of propylene resin |
| US20040108616A1 (en) * | 2002-04-26 | 2004-06-10 | Andreas Beckmann | Method for producing a foamable plastic |
| US9018269B2 (en) | 2007-11-12 | 2015-04-28 | Kaneka Corporation | Process for producing expanded polyolefin resin particles and expanded polyolefin resin particles |
| US8513317B2 (en) | 2007-12-11 | 2013-08-20 | Kaneka Corporation | Process for producing expanded polyolefin resin particles and expanded polyolefin resin particles |
| US8901182B2 (en) | 2007-12-11 | 2014-12-02 | Kaneka Corporation | Process for producing expanded polyolefin resin particles and expanded polyolefin resin particles |
| US9216525B2 (en) | 2007-12-11 | 2015-12-22 | Kaneka Corporation | Process for producing expanded polyolefin resin particles and expanded polyolefin resin particles |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0429091A2 (en) | 1991-05-29 |
| DE69022814D1 (en) | 1995-11-09 |
| EP0429091B1 (en) | 1995-10-04 |
| EP0429091A3 (en) | 1992-02-26 |
| DE69022814T2 (en) | 1996-05-23 |
| CA2030754A1 (en) | 1991-05-25 |
| KR0157621B1 (en) | 1998-12-01 |
| KR910009803A (en) | 1991-06-28 |
| CA2030754C (en) | 1997-06-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5122545A (en) | Production method of prefoamed synthetic resin particles | |
| US4308352A (en) | Process of extruding polysulfone foam | |
| US5130341A (en) | Process for the production of foamed poymer particles | |
| US5391581A (en) | Production method of foamed particles of uncrosslinked ethylene-based resin | |
| US4948817A (en) | Pre-foamed particles of uncrosslinked, linear low-density polyethylene and production method thereof | |
| JP3279382B2 (en) | Non-crosslinked polyethylene resin foam particles and method for producing the same | |
| JP3195676B2 (en) | Method for producing expanded polyolefin resin particles | |
| JP2004263033A (en) | In-mold foam molding of polyolefin-based resin | |
| JPH0386736A (en) | Production of foamed polyolefin resin particle | |
| US6133331A (en) | Expanded particles of polyolefin resin and process for preparing the same | |
| US3385804A (en) | Foamable polystyrene compositions containing fatty acid amide lubricants | |
| JPH05163381A (en) | Production of expanded polymer particle | |
| JP3281904B2 (en) | Expanded polypropylene resin particles and molded article thereof | |
| JP2874772B2 (en) | Method for producing expanded polymer particles | |
| JPH059329A (en) | Production of crosslinked expanded polyolefinic resin particle | |
| KR960003822B1 (en) | Method for manufacturing polypropylene expandable particle | |
| JP2826769B2 (en) | Method for producing expanded polymer particles | |
| JPH0386737A (en) | Production of foamed polyolefin resin particle | |
| JP2002533505A (en) | Expanded propylene polymer beads | |
| JP3526660B2 (en) | In-mold foaming particles and in-mold foam molding | |
| US5077322A (en) | Foams based on an olefin copolymer | |
| JP3198469B2 (en) | Expanded polyolefin resin particles and method for producing the same | |
| JP3195675B2 (en) | Method for producing expanded polyolefin resin particles | |
| JPH04359037A (en) | Production of synthetic resin foam granules | |
| JP3218333B2 (en) | Expanded polyolefin resin particles and method for producing the same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: JSP CORPORATION, 1-1, UCHISAIWAI-CHO 2-CHOME, CHIY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:KUWABARA, HIDEKI;SASAKI, HIDEHIRO;NAITO, MASATO;AND OTHERS;REEL/FRAME:005551/0481 Effective date: 19901113 |
|
| STCF | Information on status: patent grant |
Free format text: PATENTED CASE |
|
| FEPP | Fee payment procedure |
Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
| FPAY | Fee payment |
Year of fee payment: 4 |
|
| FPAY | Fee payment |
Year of fee payment: 8 |
|
| FPAY | Fee payment |
Year of fee payment: 12 |